CN204114898U - Supercritical CFB Boiler reheat steam temperature adjustment System - Google Patents
Supercritical CFB Boiler reheat steam temperature adjustment System Download PDFInfo
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- CN204114898U CN204114898U CN201420587031.7U CN201420587031U CN204114898U CN 204114898 U CN204114898 U CN 204114898U CN 201420587031 U CN201420587031 U CN 201420587031U CN 204114898 U CN204114898 U CN 204114898U
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- 238000012935 Averaging Methods 0.000 abstract description 6
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- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 3
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- 238000005516 engineering process Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
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- 238000005507 spraying Methods 0.000 description 2
- 241000883990 Flabellum Species 0.000 description 1
- 235000019738 Limestone Nutrition 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000011217 control strategy Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000001351 cycling effect Effects 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000003009 desulfurizing effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
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- 238000003303 reheating Methods 0.000 description 1
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Abstract
The utility model discloses a kind of Supercritical CFB Boiler reheat steam temperature adjustment System.This Supercritical CFB Boiler reheat steam temperature adjustment System comprises many group reheat steam temperature adjusting devices, each group reheat steam temperature adjusting device comprises cyclone separator, material returning device and external bed, in this external bed, there is high temperature reheater, the isolated material of cyclone separator enters material returning device, material in material returning device is divided into two parts, and wherein a part passes through this external bed to heat reheated steam.The porch of high temperature reheater is also furnished with attemperator.By controlling to adjust reheat steam temperature through the quantity of the material of external bed and attemperator.The utility model, when performing above-mentioned control, has not only been considered the various factor affecting reheat steam temperature adjustment, and has been reflected the demand of real-time working condition by the mode adding feedforward in time.The utility model also by but small oscillations Signal averaging in the control signal of the valve of material returning device, prevent valve bite.
Description
Technical field
The utility model relates to Supercritical CFB Boiler field, particularly, relates to a kind of Supercritical CFB Boiler reheat steam temperature adjustment System.
Background technology
Supercritical unit refers to that superheater outlet main steam pressure is more than 22.129MPa.Think in theory, when the state parameter of water reaches critical point (pressure 22.129MPa, temperature 374 DEG C), the vaporization completely of water can complete in a flash.Supercritical once-through boiler does not have drum, and start and stop speed is fast.Compared with the thermal efficiency of the subcritical fired power generating unit of same capacity, adopt supercritical parameter efficiency can be improved 2%-2.5% in theory.
Recirculating fluidized bed (CFB) is the high-efficiency low-pollution clean-burning technology of new generation grown up in the world in recent years, its main feature is that fuel and desulfurizing agent are through repeatedly circulating, carrying out low-temperature burning and desulphurization reaction repeatedly, in stove, turbulent motion is strong, not only can reach low NOx drainage, realize up to 90% desulfuration efficiency and the efficiency of combustion close with coal-powder boiler, and have that fuel tolerance is wide, load adjustment ability good, lime-ash is easy to the advantages such as comprehensive utilization, therefore obtain business promotion rapidly in the world.
Supercritical steam cycle Fluidized Bed Boiler (Supercritical CFB Boiler) combines both advantage, can export the superheated steam of HTHP, also have excellent environmental emission characteristic.But the combustion process due to Supercritical CFB Boiler be one have strong jamming, non-linear, time become, the process that is associated of multivariable, its Combustion System is complicated more than conventional pulverized-coal stove.The wherein adjustment of reheat steam temperature is one of difficult point of whole Supercritical CFB Boiler control.
The change of reheat steam temperature can affect the economical and security of the cycling hot of generating set, reduces service life and the thermal efficiency of equipment, even may cause serious security incident.Current bed temperature controls and reheat steam temperature adjustment is often coupled, be unfavorable for stably by Switching Logic Control of Reheat Steam Temperature in target zone.Meanwhile, owing to needing to consider multiple factor affecting reheat steam temperature, make the decision-making time longer, have certain time-delay between regulation and control and actual condition, this is also a difficult problem in the adjustment of current reheat steam temperature.
Utility model content
The purpose of this utility model is to provide a kind of Supercritical CFB Boiler reheat steam temperature adjustment System, and this system can adjust reheat steam temperature independently, makes it not control to be coupled with bed temperature, and reheat steam temperature can be made to adjust fast in response to actual condition demand.
To achieve these goals, the utility model provides a kind of Supercritical CFB Boiler reheat steam temperature adjustment System, this Supercritical CFB Boiler reheat steam temperature adjustment System comprises many group reheat steam temperature adjusting devices, each organizes described reheat steam temperature adjusting device, and to comprise the steelframe being disposed in burner hearth both sides secondary across interior cyclone separator, be disposed in the material returning device under described cyclone separator and external bed, in described external bed, there is high temperature reheater, the isolated material of described cyclone separator enters described material returning device, material in described material returning device is divided into two parts, a part directly returns the burner hearth of described Supercritical CFB Boiler, another part is by returning described burner hearth after described external bed.
Preferably, system comprises 2 groups of reheat steam temperature adjusting devices, lays respectively at the left and right sides of furnace front, the reheat steam temperature of the reheat steam temperature adjusting device adjustment burner hearth left part in left side, the reheat steam temperature of the reheat steam temperature adjusting device adjustment burner hearth right part on right side.
Preferably, material returning device has the first valve, and the aperture of the first valve can be conditioned, to regulate the material that directly returns burner hearth in material returning device and the ratio by the material that returns burner hearth after external bed.
Preferably, Supercritical CFB Boiler reheat steam temperature adjustment System also comprises oscillator, and the oscillator signal that oscillator produces is applied in the input signal of the control end of the first valve.
Preferably, reheat steam temperature adjusting device also comprises the attemperator of the porch being disposed in high temperature reheater, and attemperator has the second valve.
By technique scheme, the temperature of the utility model by regulating the amount entering the material of external bed from material returning device to control the reheated steam by the high temperature reheater external bed, to control reheat steam temperature.Also by arranging attemperator (i.e. emergency spray device) in the porch of high temperature reheater, to adjust reheat steam temperature further.When controlling the valve opening of the valve opening of material returning device and attemperator, not only considering the various factor affecting reheat steam temperature adjustment, and having been reflected the demand of real-time working condition by the mode adding feedforward in time.The utility model also by but small oscillations Signal averaging in the control signal of the valve of material returning device, prevent valve bite.
Other feature and advantage of the present utility model are described in detail in detailed description of the invention part subsequently.
Accompanying drawing explanation
Accompanying drawing is used to provide further understanding of the present utility model, and forms a part for description, is used from explanation the utility model, but does not form restriction of the present utility model with detailed description of the invention one below.In the accompanying drawings:
Fig. 1 is the schematic diagram according to one group of reheat steam temperature adjusting device in the Supercritical CFB Boiler reheat steam temperature adjustment System of a kind of preferred embodiment of the present utility model;
Fig. 2 is the flow chart regulating the first valve opening in the Supercritical CFB Boiler reheat steam temperature method of adjustment according to a kind of preferred embodiment of the present utility model;
Fig. 3 is the flow chart regulating the second valve opening in the Supercritical CFB Boiler reheat steam temperature method of adjustment according to a kind of preferred embodiment of the present utility model; And
Fig. 4 is the example block diagram in the left part reheat steam temperature adjustment loop in the embodiment according to Fig. 2 and Fig. 3.
Detailed description of the invention
Below in conjunction with accompanying drawing, detailed description of the invention of the present utility model is described in detail.Should be understood that, detailed description of the invention described herein, only for instruction and explanation of the utility model, is not limited to the utility model.
In the utility model, when not doing contrary explanation, burner hearth afterbody refers to the position of burner hearth near flue, and furnace front refers to the position away from flue.The technical term that term " summing point ", " PID ", " little choosing " are automation field.
In a kind of boiler of the Supercritical CFB Boiler reheat steam temperature adjustment System adopting the utility model to provide, one time vapour can successively through low temperature superheater, one-level water injector, medium temperature overheater I, secondary water injector, medium temperature overheater II, three grades of water injectors and high temperature superheater in heating process.Secondary vapour can pass through low-temperature reheater, emergency spray device, high temperature reheater successively in heating process.Whether each water injector starts is determined on a case-by-case basis.Ideally, the entrance and exit temperature of low temperature superheater is respectively 430 DEG C and 471 DEG C; The entrance and exit temperature of medium temperature overheater I is respectively 461 DEG C and 496 DEG C; The entrance and exit temperature of medium temperature overheater II is respectively 483 DEG C and 520 DEG C; The entrance and exit temperature of high temperature superheater is respectively 510 DEG C and 570 DEG C; The entrance and exit temperature of low-temperature reheater is respectively 317 DEG C and 484 DEG C; The entrance and exit temperature of high temperature reheater is respectively 484 DEG C and 569 DEG C.
The utility model provides a kind of Supercritical CFB Boiler reheat steam temperature adjustment System, this Supercritical CFB Boiler reheat steam temperature adjustment System comprises many group reheat steam temperature adjusting devices, it is secondary across interior cyclone separator that each group reheat steam temperature adjusting device comprises the steelframe being disposed in burner hearth both sides, be disposed in the material returning device under cyclone separator and external bed, in external bed, there is high temperature reheater, the isolated material of cyclone separator enters material returning device, material in material returning device is divided into two parts, a part directly returns the burner hearth of Supercritical CFB Boiler, another part is by returning burner hearth after external bed.
Fig. 1 is the schematic diagram according to one group of reheat steam temperature adjusting device in the Supercritical CFB Boiler reheat steam temperature adjustment System of a kind of preferred embodiment of the present utility model.Reheat steam temperature adjustment System in present embodiment comprises 2 groups of reheat steam temperature adjusting devices, often organize reheat steam temperature adjusting device and comprise a cyclone separator 12, material returning device 13 and an external bed 14, wherein cyclone separator 12 is disposed in the steelframe pair of burner hearth 11 both sides across interior, material returning device 13 and external bed 14 are disposed in cyclone separator 12 times, and high temperature reheater is disposed in external bed 14.2 groups of reheat steam temperature adjusting devices lay respectively at the left and right sides of burner hearth 11 front portion.And in the present embodiment, left side reheat steam temperature is controlled by the one group of reheat steam temperature adjusting device be positioned on the left of burner hearth, right side reheat steam temperature is controlled by the one group of reheat steam temperature adjusting device be positioned on the right side of burner hearth, left side and the adjustment of right side reheat steam temperature are not coupled, and partially burn and occur that thermic load is uneven to avoid burner hearth as far as possible.One group that illustrate only wherein briefly herein to make diagram, another group structure is similar, and only installation site is different.
As shown in Figure 1, coal and lime stone etc. complete burning and desulphurization reaction in burner hearth 11, and the flue gas of generation is discharged to cyclone separator 12.Cyclone separator 12 is connected with corresponding material returning device 13 with back-end ductwork (not shown).Cyclone separator 12 carries out gas-solid two phases to the flue gas entered, and the flue gas after purification is discharged to back-end ductwork (not shown), and isolated high-temperature material then enters material returning device 13.Material in material returning device 13 is divided into two parts, and wherein a part directly returns burner hearth, and another part is introduced into external bed 14, with the heating surface generation heat exchange of the high temperature reheater in external bed 14 to heat reheated steam, and then returns burner hearth 11.Material returning device 13 can have valve 15 (can be described as the first valve).Valve 15 can be cone valve.Regulate the quantity of the material sending into external bed 14 by control valve 15, thus regulate the temperature of the high temperature reheated steam generated.
In operation, if combustion position and load condition keep stable for a long time, valve 15 may be caused due to not operating for a long time and by bite.Therefore, according to this preferred embodiment, but small oscillations signal is generated by oscillator, and by this but small oscillations Signal averaging to the control signal of valve 15, make containing oscillator signal component in the input signal of the control end finally inputting valve 15, regularly or aperiodically to drive valve 15 small size action to occur to avoid by bite.Such as, if the amplitude of valve 15 standard-sized sheet is 100%, can be 2% by an amplitude, the action reciprocating vibration Signal averaging that is spaced apart 300 seconds is to the control signal of valve 15.Now, suppose the aperture of 50% can be kept according to unit load and combustion case etc. constant in a very long time inner valve 15, owing to there is oscillator signal component in the input signal of control end, therefore can by fine setting to aperture 52% every 300 seconds late gates, 50% is recalled to again every 300 seconds, finely tuned to 48% after next 300 seconds, then recalled to 50% after 300 seconds, moved in circles.Equally, this oscillator signal also can be nonperiodic signal.The amplitude of oscillator signal can be arranged according to actual conditions.
Preferably, can arrange that there is attemperator 16 (i.e. emergency spray device) at the entrance of high temperature reheater, such as, can respectively arrange an attemperator 16, to adjust reheat steam temperature further in each high temperature reheater entrance both sides.When reheat steam temperature too high and only regulate send into the material quantity of external bed 14 be difficult in a short time prove effective time, spray water the vapor (steam) temperature entering high temperature reheater is reduced rapidly by controlling attemperator 16.Attemperator 16 can have valve 17 (can be called as the second valve).
Fig. 2 is the flow chart of the Supercritical CFB Boiler reheat steam temperature method of adjustment according to a kind of preferred embodiment of the present utility model.
In S1, desirable reheat steam temperature value, additional adjusted value and the first high temperature reheater outlet temperature corresponding according to the first load can determine the first aperture.First load and the first high temperature reheater outlet temperature refer to boiler load and the high temperature reheater outlet temperature of moment t1.By to table look-up or the method such as function curve mapping obtains the desirable reheat steam temperature value corresponding to the first load.Meanwhile, operator can provide an additional adjusted value as required.Desirable reheat steam temperature value and additional adjusted value can be used as the input of summing point, and the output of summing point can be used as reheat steam temperature setting value.In some cases, if wish that reheat steam temperature setting value is completely given by operator, desirable reheat steam temperature value corresponding for the first load can be set as 0 DEG C.Such as, for certain 600MW (megawatt) Supercritical CFB Boiler, if boiler load is 383.32MW, if wish that the first load does not have an impact to the first aperture, desirable reheat steam temperature value corresponding to any first load all can be set to 0 DEG C, now operator according to circumstances can provide additional adjusted value is 558.00 DEG C, then the reheat steam temperature setting value that summing point exports is 558.00 DEG C.If the high temperature reheater outlet temperature now recorded is 558.62 DEG C, can by reheat steam temperature setting value 558.00 DEG C and high temperature reheater outlet temperature 558.62 DEG C input PID adjuster.In present embodiment, PID also can be set as required and regulate dead band.PID adjuster can obtain corresponding valve (such as, cone valve) aperture according to two temperature values of input, and this valve opening can be called as the first aperture.Such as, because high temperature reheater outlet temperature is now higher than reheat steam temperature setting value, the first aperture therefore obtained is negative value, such as can for-15.02% (aperture when setting the first valve wide open as 100%).Summing point and PID adjuster can be hardware circuits also can be software program.Additional adjusted value also can be on the occasion of, zero or negative value.
In S2, can according to the second load determine as feedforward the second aperture.Complete a series of process in S1 (particularly PID regulates) and need certain hour, if using the first aperture of obtaining in S1 directly as the control signal of the first valve, control signal can be made to lag behind real-time working condition.Therefore can according to the Real-time Load (i.e. the second load) at moment t2 by table look-up or the method such as function curve mapping obtains the first valve (such as cone valve) second aperture as feedforward.Such as, from t1 to t2, boiler load becomes 383.18MW from 383.32MW, and caning be passed through estimation (such as, by tabling look-up or the method such as simple computation) the second aperture obtained corresponding to the second load 383.18MW is 32.65%.Second aperture is a comparatively "ball-park" estimate value, but has short advantage computing time, can reflect the up-to-date load condition of boiler in time.
In S3, determine the 3rd aperture according to the first aperture and the second aperture.Such as, can using the input as summing point of acquired first aperture and the second aperture, it exports as the 3rd aperture.3rd aperture can be used for control the 3rd aperture.Such as, continue with reference to above example, the first aperture is the-15.02%, the second aperture is 32.65%, and can obtain the 3rd aperture is 17.63%.Both considered in the acquisition process of the 3rd aperture may affect reheat steam temperature adjustment multiple factors (such as, desirable reheat steam temperature value, additional adjusted value and high temperature reheater outlet temperature), consider again the Real-time Load of boiler, and be absorbed in reheat steam temperature adjustment, therefore have accurately, stable and feature fast.
Preferably, in S4, upper and lower amplitude limit can be carried out to the 3rd aperture.Such as, can float the second aperture 30% and the bound of the value after 30% as amplitude limit of floating downward.In upper example, the second aperture is 32.65%%, then the scope of amplitude limit can be [62.65%%, 2.65%%] up and down.In above-mentioned example, the 3rd aperture is 17.63%, and this value is in scope [62.65%%, 2.65%%], and the output valve therefore after amplitude limit is still 17.63%.
Preferably, in S5, the Signal averaging but small oscillations signal after amplitude limit can be given.Such as, the but small oscillations signal that the signal after amplitude limit and oscillator produce can be delivered to summing point, its output can be sent to the input of the first valve.This oscillator signal can drive the regular or small size action of irregular generation of the first valve, to prevent the first valve bite that may cause owing to being failure to actuate for a long time.Such as, the amplitude of this oscillator signal can be about 2% of the amplitude of the first valve wide open.
In S6, the aperture of Signal Regulation first valve exported with S5, to control the quantity of the material sending into external bed, thus the reheat steam temperature of adjustment Supercritical CFB Boiler.Such as, if reheat steam temperature is higher, then can the quantity of material of less input external bed; Vice versa.
Fig. 3 is the flow chart regulating the second valve opening in the Supercritical CFB Boiler reheat steam temperature method of adjustment according to a kind of preferred embodiment of the present utility model.
In S7, the 4th aperture can be determined according to additional adjusted value and the second high temperature reheater outlet temperature.If additional adjusted value is now still 558.00 DEG C, high temperature reheater outlet temperature is still 558.62 DEG C, can by one a little more than (such as, high 5 DEG C) temperature value of additional adjusted value 563.00 DEG C and high temperature reheater outlet temperature send into PID adjuster, and the output of this PID adjuster can be the 4th aperture.The temperature value a little more than additional adjusted value is selected to be just start water spray where necessary in order to ensure attemperator.Because desuperheater spray can cause the steam temperature of the secondary vapour entering high temperature reheater to reduce rapidly, if on the low side may the making of this steam temperature contains aqueous water in the final high temperature reheating gas exported, the flabellum etc. of steam turbine is caused damage.So usually select comparatively conservative attemperator control strategy.Such as, the temperature value inputting this PID adjuster is 563.00 DEG C and 558.62 DEG C, then the 4th aperture now obtained is 0%.
In S8, the 5th aperture can be determined according to main steam flow.By to table look-up or the method such as Function Mapping obtains the 5th aperture corresponding to main steam flow.
In S9, the 4th aperture and the 5th aperture can be compared, select wherein less aperture as the control signal of the second valve.Aperture represented by this control signal is larger, then the injection flow rate of attemperator is larger, more remarkable to the cooling effect of reheat steam temperature; Otherwise the aperture represented by this control signal is less is even zero, then injection flow rate is less or do not spray water, less on the impact of reheat steam temperature.Equally, in working control, if due to the temperature of reheated steam deviating on the low side, may cause in reheated steam containing aqueous water, steam turbine is caused damage, therefore perform in S9 and littlely select principle, with avoid the transient state burr etc. due to temperature value cause desuperheater spray amount bigger than normal or when unnecessary water spray water spray and make the temperature of reheated steam deviating on the low side.
In S10, whether to open by regulating the second valve or it opens aperture, control attemperator whether to spray water or the water yield of spraying water, thus adjust rapidly the reheat steam temperature of Supercritical CFB Boiler when reheat steam temperature is too high and other regulating measures are difficult to prove effective in a short time.In upper example, because the 4th aperture is 0%, therefore no matter why the 5th aperture is worth, and attemperator all keeps state of not spraying water.
Preferably, independent control can be carried out to the left part reheat steam temperature of Supercritical CFB Boiler and right part reheat steam temperature, to avoid because combustion case difference causes burner hearth partially to burn.Now, when adjusting reheat steam temperature on the left of burner hearth, in said method, all high temperature reheater outlet temperatures related to are the outlet steam temperature of the high temperature reheater on the left of the burner hearth that records in the corresponding moment, and the final signal exported is for regulating the first valve and the second valve that are arranged in the reheat steam temperature adjusting device on the left of burner hearth in Supercritical CFB Boiler reheat steam temperature adjustment System; Vice versa.Left side and the adjustment of right side reheat steam temperature are not coupled each other.
Fig. 4 is the example block diagram in the reheat steam temperature adjustment loop, left side according to a kind of preferred embodiment of the present utility model.Boiler load instruction is sent to load-temperature map block 31, and load-temperature map block 31 exports the desirable reheat steam temperature value corresponding to this load (i.e. the first load).The additional adjusted value that operator provides and the desirable reheat steam temperature value that load-temperature map block 31 exports are input to summing point 32, and the output of summing point 32 can be counted as reheat steam temperature setting value.This reheat steam temperature setting value and the left side high temperature reheater outlet temperature recorded are transfused to PID adjuster 33, to obtain the first aperture of valve.Now, also can from aperture estimate block 34 obtain as feedforward the second aperture.The input that valve degree estimates block 34 is real-time boiler load instruction (namely corresponding to the instruction of the second load).Then the first aperture and the second aperture are all sent to summing point 35, and its output can be used as the 3rd aperture.In present embodiment, preferably, also by clip block 36, amplitude limit is carried out to the 3rd aperture.Amplitude when being then the first valve wide open to the Signal averaging amplitude after amplitude limit in summing point 37 2% oscillator signal.This oscillator signal can be produced by oscillator 38.The signal that summing point 37 exports can be used as the input that input signal is input to the valve 39 of material returning device, to regulate the aperture of the first valve, thus regulates the quantity of the material entering the external bed being arranged high temperature reheater from material returning device.On the other hand, input to PID adjuster 41 after additional adjusted value is increased 5 DEG C in temperature adjustment block 40, the output that high temperature reheater outlet temperature is also input to PID adjuster 41, PID adjuster 41 is the 4th aperture.Main steam flow obtains the 5th corresponding aperture after steam flow amount-aperture mapping block 42.From the 4th and the 5th aperture, select less aperture little choosing in block 43, control the second valve 44 of attemperator as control signal.In present embodiment, what be positioned at the porch of the high temperature reheater on the left of burner hearth is each side furnished with an attemperator, and these two attemperators valve 44 is separately controlled by same signal.
Below preferred embodiment of the present utility model is described by reference to the accompanying drawings in detail, but, the utility model is not limited to the detail in above-mentioned embodiment, within the scope of technical conceive of the present utility model, multiple simple variant can be carried out to the technical solution of the utility model, such as change clipping range, the amplitude of different oscillator signals and cycle etc. are set, if or wish only to control attemperator according to additional adjusted value and high temperature reheater outlet temperature, the 5th corresponding for any main steam flow aperture all can be set to 100%.These simple variant all belong to protection domain of the present utility model.
It should be noted that in addition, each the concrete technical characteristic described in above-mentioned detailed description of the invention, in reconcilable situation, can be combined by any suitable mode.In order to avoid unnecessary repetition, the utility model illustrates no longer separately to various possible combination.
In addition, also can be combined between various different embodiment of the present utility model, as long as it is without prejudice to thought of the present utility model, it should be considered as content disclosed in the utility model equally.
Claims (5)
1. a Supercritical CFB Boiler reheat steam temperature adjustment System, it is characterized in that, this Supercritical CFB Boiler reheat steam temperature adjustment System comprises many group reheat steam temperature adjusting devices, each organizes described reheat steam temperature adjusting device, and to comprise the steelframe being disposed in burner hearth both sides secondary across interior cyclone separator, be disposed in the material returning device under described cyclone separator and external bed, in described external bed, there is high temperature reheater, the isolated material of described cyclone separator enters described material returning device, material in described material returning device is divided into two parts, a part directly returns the burner hearth of described Supercritical CFB Boiler, another part is by returning described burner hearth after described external bed.
2. Supercritical CFB Boiler reheat steam temperature adjustment System according to claim 1, it is characterized in that, described system comprises reheat steam temperature adjusting device described in 2 groups, lay respectively at the left and right sides of described furnace front, the described reheat steam temperature adjusting device in left side adjusts the reheat steam temperature of described burner hearth left part, and the described reheat steam temperature adjusting device on right side adjusts the reheat steam temperature of described burner hearth right part.
3. Supercritical CFB Boiler reheat steam temperature adjustment System according to claim 1, it is characterized in that, described material returning device has the first valve, the aperture of described first valve can be conditioned, to regulate the material that directly returns described burner hearth in described material returning device and the ratio by the material that returns described burner hearth after described external bed.
4. Supercritical CFB Boiler reheat steam temperature adjustment System according to claim 3, it is characterized in that, described Supercritical CFB Boiler reheat steam temperature adjustment System also comprises oscillator, and the oscillator signal that described oscillator produces is applied in the input signal of the control end of described first valve.
5. Supercritical CFB Boiler reheat steam temperature adjustment System according to claim 1, it is characterized in that, described reheat steam temperature adjusting device also comprises the attemperator of the porch being disposed in described high temperature reheater, and described attemperator has the second valve.
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| CN201420587031.7U CN204114898U (en) | 2014-07-15 | 2014-10-11 | Supercritical CFB Boiler reheat steam temperature adjustment System |
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| CN201410336125.1 | 2014-07-15 | ||
| CN201420587031.7U CN204114898U (en) | 2014-07-15 | 2014-10-11 | Supercritical CFB Boiler reheat steam temperature adjustment System |
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| CN104266164A (en) * | 2014-07-15 | 2015-01-07 | 神华集团有限责任公司 | Supercritical CFB (Circulating Fluidized Bed) boiler reheating steam temperature adjusting system and adjusting method |
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| CN104896166A (en) * | 2015-05-27 | 2015-09-09 | 国网山西省电力公司电力科学研究院 | Electric control adjusting system of conical valve of circulating fluidized bed boiler external type heat exchanger |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5784975A (en) * | 1996-12-23 | 1998-07-28 | Combustion Engineering, Inc. | Control scheme for large circulating fluid bed steam generators (CFB) |
| CN101666495A (en) * | 2009-09-03 | 2010-03-10 | 昆明理工大学 | Method for controlling material return quantity of hearth of circulating fluidized bed boiler |
| CN101968215A (en) * | 2010-11-17 | 2011-02-09 | 上海锅炉厂有限公司 | Arrangement structure of subcritical circulating fluidized bed boiler |
| CN102095195B (en) * | 2011-01-11 | 2013-04-17 | 清华大学 | Reburning type circulating fluidized bed boiler |
| CN104266164B (en) * | 2014-07-15 | 2017-08-25 | 神华集团有限责任公司 | Supercritical CFB Boiler reheat steam temperature adjusts system and method for adjustment |
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2014
- 2014-10-11 CN CN201410535120.1A patent/CN104266164B/en active Active
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104266164A (en) * | 2014-07-15 | 2015-01-07 | 神华集团有限责任公司 | Supercritical CFB (Circulating Fluidized Bed) boiler reheating steam temperature adjusting system and adjusting method |
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| CN104266164A (en) | 2015-01-07 |
| CN104266164B (en) | 2017-08-25 |
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